EP1885660B1 - Pelletierung von kalkfeingut mit asphaltverbessernden bindemitteln und verfahren zur verwendung bei der asphaltherstellung - Google Patents
Pelletierung von kalkfeingut mit asphaltverbessernden bindemitteln und verfahren zur verwendung bei der asphaltherstellung Download PDFInfo
- Publication number
- EP1885660B1 EP1885660B1 EP06760293.8A EP06760293A EP1885660B1 EP 1885660 B1 EP1885660 B1 EP 1885660B1 EP 06760293 A EP06760293 A EP 06760293A EP 1885660 B1 EP1885660 B1 EP 1885660B1
- Authority
- EP
- European Patent Office
- Prior art keywords
- lime
- pellet
- asphalt
- pellets
- binder
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Active
Links
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Images
Classifications
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L97/00—Compositions of lignin-containing materials
-
- C—CHEMISTRY; METALLURGY
- C08—ORGANIC MACROMOLECULAR COMPOUNDS; THEIR PREPARATION OR CHEMICAL WORKING-UP; COMPOSITIONS BASED THEREON
- C08L—COMPOSITIONS OF MACROMOLECULAR COMPOUNDS
- C08L95/00—Compositions of bituminous materials, e.g. asphalt, tar, pitch
-
- Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
- Y10—TECHNICAL SUBJECTS COVERED BY FORMER USPC
- Y10T—TECHNICAL SUBJECTS COVERED BY FORMER US CLASSIFICATION
- Y10T428/00—Stock material or miscellaneous articles
- Y10T428/29—Coated or structually defined flake, particle, cell, strand, strand portion, rod, filament, macroscopic fiber or mass thereof
- Y10T428/2982—Particulate matter [e.g., sphere, flake, etc.]
Definitions
- the present invention relates to lime pellets for use in asphalt applications. More particularly, the present invention relates to compositions and methods of manufacturing lime pellets, and methods of using lime pellets in asphalt manufacturing and paving.
- Asphalt pavements are well-known and have been used for many years.
- an asphalt pavement includes an aggregate and asphalt cement mixed together in what is commonly referred to as hot mix asphalt (HMA).
- HMA hot mix asphalt
- the asphalt cement is a hydrocarbon-rich substance such as, or prepared from, bitumen, and is used to bind the aggregate into a pavement.
- the type and amount of aggregate can vary, and it provides structural reinforcement and durability to the HMA.
- the asphalt cement functions as a continuous phase that binds the aggregate materials together, it is well known that various additives such as lime can be used to improve the durability and longevity of asphalt pavements.
- lime fines have been used in treating HMA ingredients in order to improve the long-term interactions or bonds between the asphalt cement and aggregate.
- Such improvements have included anti-strip characteristics and reduced deformation or softening of the asphalt pavement over time.
- These improvements have been obtained by either combining the lime fines with the aggregate or with the asphalt cement before the aggregate and asphalt cement have been prepared into hot mix asphalt. It is thought, without being bound thereto, that lime improves the physical characteristics of the asphalt pavement by inhibiting any absorbed water from softening the pavement, and/or by enhancing the physical interface and bonding between the aggregates and the asphalt cement.
- the lime fines have been added in bulk to one of the hot mix asphalt ingredients by well-known methodologies and techniques. More particularly, the powdered lime can be supplied by inline injection, or bulk dumping. While favorable asphalt pavement characteristics can be obtained by the current methodologies, problems have arisen from the lime fines clumping or becoming airborne, which jeopardizes the ability to accurately measure or control the amount of lime being used.
- lime fines to marinate the aggregate has also caused other health-related complications. This is because the powdered lime fines are usually combined with the aggregate and allowed to sit on the ground for weeks or months. As a result, the lime fines have leached into the groundwater and flowed into neighboring aquifers. The presence of lime fines in the water kills fish, and can contaminate drinking water.
- lime fines has caused problems with manufacturing and construction equipment. Again, this is at least partially a consequence of the small particulate nature of such lime fines (e.g., smaller than 200 mesh), which allows clouds of the particulates to float or circulate around construction sites and asphalt manufacturing facilities.
- the small particulates eventually deposit on the machinery or equipment and become entrained within joints and other moving parts. The particles cause excessive wear and fatigue, and result in the equipment wearing out prematurely.
- problems have arisen from the lime fines being sucked into the bags of baghouses so as to foul the bags and render them unusable.
- the present invention has been developed in response to the present state of the art, and in particular, in response to problems and needs that have not been solved.
- a hot melt asphalt pellet comprises:
- the present invention includes a lime pellet for use in asphalt manufacturing.
- the pellet is comprised of lime fines such as calcium hydroxide (Ca(OH) 2 ) fines and/or calcium oxide (CaO) fines, and an asphalt-compatible binder.
- the asphalt-compatible binder is mixed with the lime in an amount and disposition sufficient to form a pellet, wherein the pellet is characterized as having a rigid structure with a dimension greater than about 1.5 mm (about 0.05 inch).
- the lime pellet is compatible with a hot mix asphalt and/or asphalt cement and dissolvable in liquid asphalt.
- a method of manufacturing of the lime pellet of the first aspect comprises:
- embodiments of the present invention are directed to the production and use of lime-based pellets for modifying asphalt compositions and pavements.
- the terminology employed herein is used for the purpose of describing particular embodiments only and is not intended to be limiting.
- fines is meant to refer to the small particulate nature of the lime powders used in hot asphalt mix production. As such, the lime fines are small, finely divided, and light weight particulates that are easily airborne when handled or exposed to minimal air currents.
- the term "storage-stable” is meant to refer to a physical characteristic that inhibits or prevents a pellet from degrading or combining with adjacent pellets under ambient conditions. That is, when under normal ambient conditions at a normal humidity, the pellets are form-stable. As such, when a plurality of storage-stable pellets are piled in storage, the individual pellets retain their distinct structural integrity without forming an agglomeration of pellets.
- the lime-based pellets are prepared in a manner that binds lime fines into an asphalt-compatible binder.
- Embodiments of the methods for manufacturing lime pellets according to the present invention comprise mixing lime with an asphalt-compatible binder such as bitumen, tall oil pitch, lignosulfonate , and subsequently forming pellets in the shape of pastilles, slates, chips, briquettes, or other small forms of the asphalt pavement conditioning and binding product.
- the resulting pellets are suitable for storage and transportation at a wide range of ambient temperatures because of their rigid and non-flow properties.
- the pellets can be stored at the production site or at a remote site and can be transported and stored in piles or within containers such as sacks, tanks, and barrels.
- the ability to store the pellets without degradation or agglomeration permits the accumulation of large quantities of pellets and shipment in large quantities to remote locations.
- the properties of the various embodiments of lime-based pellets according to the present invention are such that the pellets can effectively be shipped over long distances, such as by transatlantic and transcontinental shipments, by any one of a variety of conventional means, such as rail cars, trucks, ships, and airplane.
- Properties that facilitate the storage and shipment of the inventive lime-based pellets in large quantities include the rigid, non-sticky, non-aggregating, and non-flow properties that enable handling without the concerns associated with fines or particulates becoming airborne.
- the individual pellets are storage-stable so as to not agglomerate with adjacent pellets.
- an individual pellet does not substantially degrade or agglomerate with adjacent pellets for a duration longer than about 30 days, more preferably longer than about 60 days, and most preferably longer than about 90 days.
- some pellet configurations can be form-stable for longer than about 6 months or longer than about 12 months. As such, when pellets are stored at normal or natural ambient conditions and humidity, the individual pellets retain their form.
- Some embodiments of lime-based pellets according to the present invention are configured so as to protect asphalt pavement against water-induced detrimental effects, thus preventing or reducing undesirable effects that sometimes occur due to long-term exposure to precipitation such as rain, snow, and/or ice. Also, the pellets can prevent or inhibit oxidative age hardening of the asphalt pavement. Some embodiments of lime-based pellets according to the present invention are provided with components or modifiers that provide the dark or black colored asphalt pavement that is familiar and preferred.
- the lime-based pellets have a size that prevents them from becoming easily airborne due to wind currents or handling. It has been found that when the pellets are at least larger than 14 mesh so as to not pass therethrough, ease of use and handling greatly increases.
- the pellets can have a dimension greater than about 1.5 mm (about 0.05 inch) to inhibit or prevent being passed through 14 mesh, more preferably to prevent being passed through 8 mesh, and most preferably to prevent being passed through 4 mesh.
- the asphalt-compatible binder is comprised of bitumen.
- Bitumen is a generic term referring to a flammable mixture of various hydrocarbon materials derived naturally or by distillation from petroleum. Usually, bitumen has a dark brown or black color, and can be present in forms that range from sticky and/or viscous oils to brittle solids such as asphalt, tars, and natural mineral waxes. Examples of substances containing bitumen include bituminous coal, tar, pitch, or Engen Bitumen 110-2TM (Engen Petroleum Limited; South Africa).
- the pellets can include bitumen at general binder concentrations, or at a concentration ranging from about 10% to about 75%, more preferably from about 20% to about 69% or 70%, and most preferably about 25% to about 60% by total weight of the pellets.
- bitumen at 50% by total weight.
- the binder can be an asphalt cement
- asphalt cements are commonly abbreviated with the terms AC-xx.
- the notation "xx" in the description of AC asphalt represents a numeral related to the asphalt viscosity.
- Asphalts such as AC-20 and AC-10 are the preferred forms to be used as binders.
- Other forms of asphalt that are contemplated as constituents in binder formulations include AC-1.75, AC-2.5, AC-5, AC-30, AC-40, AC-80, and AC-120 asphalts.
- the super pave grading system "PG-xx-xx” e.g., PG-76-22
- PG-xx-xx can be used to identify asphalt oils, wherein the "xx” notations designate temperatures in Celsius for the performance grade.
- hydrocarbon-based materials can be used to bind lime fines.
- hydrocarbon-based materials include heavy crude oil, fuel oil, tall oil pitch.
- these materials can be added as constituents in asphalt cement formulations or bitumen compositions.
- tall oil pitch when tall oil pitch is used it can bind the lime fines at about 1% to 20% by weight of the pellet
- collagen or collagen derivatives can be used as an asphalt-compatible binder.
- Such collagen derivatives particularly suitable for preparing lime pellets can be obtained from leather production waste, wherein the collagen or derivative thereof has been reduced to polypeptides.
- the collagen derivatives can include Collagen CH 2 TM (Mars Mineral; Mars, PA).
- latex in another embodiment, can be used as an asphalt-compatible binder, and/or used as an adhesive additive.
- the benefits arise from the composition of latex, which includes an emulsion of a synthetic rubber or plastic obtained by polymerization.
- the benefits may be realized for the same reasons latex is used in coatings, paints, and adhesives.
- latex can be used within the general binder concentrations.
- latex when used as an adhesive additive by being combined with bitumen or another binder, it can be used at less than about 30% by weigh of the pellet, more preferably less than about 20% by weight, and most preferably less than 10% by total weight.
- polymers that can be used include acrylic polymers such as polymethylmethacrylate and polyethylmethacrylate, silicon-based polymers such as polydimethylsiloxane,
- acrylic polymers such as polymethylmethacrylate and polyethylmethacrylate
- silicon-based polymers such as polydimethylsiloxane
- a polymer can be used at the general binder concentrations.
- an adhesive additive it can be used at less than about 30% by weigh of the pellet, more preferably less than about 20% by weight, and most preferably less than 10% by total weight.
- rheology-modifiers include polysaccharides such as caroboxymethylcellulose, other celluloses, amyloses, inulins, chitins, chitosans, amylopectins, glycogens, pectins, hemicelluloses, glucomannans, galactoglucomannans, xyloglucans, methylglucuronoxylans, arabinoxylans, methylglucuronoarabinoxylans, glycosaminoglycans, chondroitins, hyaluronic acids, alginic acids.
- polysaccharides such as caroboxymethylcellulose, other celluloses, amyloses, inulins, chitins, chitosans, amylopectins, glycogens, pectins, hemicelluloses, glucomannans, galactoglucomannans, xyloglucans, methylglucuronoxylans, arabinoxylan
- the first mixer 16 is configured to receive a first feed of materials through a first feed line 12 and a second feed of materials through a second feed line 14.
- the first mixer 16 processes the materials supplied by the first line 12 and second line 14 into a first mixture 24.
- an optional second mixer 22 has a third feed line 18 and a fourth feed line 20 that supplies the material to be mixed into a second mixture 26.
- the first mixer 16 and/or the second mixer 18 can be configured for variable speed and shear mixing at elevated temperatures.
- the pelletizer 38 can be configured for cutting the extrudate 34 into a variety of shapes and sizes.
- the extrudate 34 can be cut into pellets having a diameter range from about 1.5 mm (about 0.05 inches) to about 2.54 cm (about 1 inch), more preferably in a range of from about 2 mm (about 0.08 inches) to about 2 cm (about 0.8 inches), even more preferably about 3 mm (about 0.1 inches) to about 1.5 cm (about 0.6 inches), and most preferably in a range of from about 6 mm (about 0.2 inches) to about 1 cm (about 0.4 inches).
- a lime feed line 102 is introduced into a lime vessel 106, where it can be mixed with an optional conditioner such as a solvent, rheology-modifier, additive, or other particulate filler material that is supplied by the optional feed line 104.
- the lime vessel 106 can include a heating element, mixing equipment, or other processing equipment for conditioning the lime fines. Otherwise, the lime fines can be supplied into the lime vessel 106 so that these can be precisely metered during the pelleting process.
- a binder feed line 108 is introduced into a binder vessel 112, where it can be mixed with an optional conditioner such as a solvent, rheology-modifier, other particulate or conditioning material, or adhesive additive supplied by the optional feed line 110.
- the binder vessel 112 can be configured to accurately meter the binder composition for preparing the pellets.
- the binder vessel 112 can be substantially similar to the lime vessel 106.
- a supply of a lime-binder composition can then be provided from the mixer 118 to a disc pelletizer 126 via line 120.
- a supply of lime can be provided by the lime vessel 106 directly to the disc pelletizer 126 via line 122.
- the lime composition resides on the disc pelletizer 126, which is rotated by a drive system 128, until a supply of binder is provided from the binder vessel 112 via line 124.
- the binder is applied drop-wise or by a slow flowing line to the lime on the disc pelletizer 126. As the binder contacts the lime, a small pellet is formed.
- the second mixing vessel 168 can be configured for rapidly increasing the temperature of the lime pellets.
- the lime pellets can be rapidly dissolved upon being introduced into the second mixing vessel 168 and upon contacting or being entrained within a liquefied asphalt cement composition.
- a second mixing vessel 168 can rapidly heat the lime pellets so that they are substantially dissolved within a timeframe of less than about 1 minute, more preferably less than about 30 seconds, even more preferably less than about 20 seconds, and most preferably less than about 10 seconds. Additionally, in certain embodiments it can be preferred that the lime pellets dissolve within about 5 seconds to about 15 seconds.
- the aggregate-lime mixture can be supplied from the mixing vessel 166 to the hot mix vessel 180 (e . g ., pugmill, drum mixer, etc.) via line 170.
- asphalt cement can be transported to the hot mix vessel 180 directly from the asphalt cement supply 156 via line 178.
- the lime pellets and aggregate can be added directly into liquefied asphalt cement and mixed so that the resulting hot mix asphalt 182 supplied from the hot mix vessel 180 has a substantially homogeneous or uniform composition.
- a schematic diagram illustrates embodiments of a bonding process 200 for binding different layers of asphalt pavement together.
- the bonding process 200 can be performed over an old or new layer of asphalt pavement 202.
- the asphalt pavement layer 202 can be an old layer of asphalt pavement that needs a topcoat or surfacing, or a new layer that has been recently deposited.
- the lime pellets 204 are applied over the asphalt pavement layer 202.
- the liquid asphalt can at least partially melt the lime pellets 204 and form a bonding layer 207.
- the bonding layer 207 can be comprised of pellet portions 208 and asphalt cement portions 210.
- the pellet portions 208 can impart the lime fines into the asphalt cement portions 210 so as to enhance the bonding between the first asphalt layer 202 and the second asphalt layer 206.
- the lime fines can also be distributed and suspended into the second asphalt layer 206.
- the lime pellets 204 can be used in facilitating and enhancing the bonding between different layers of asphalt.
- a heavy roller 212 can be used to smash or compact the lime pellets 204 into a lime layer 214.
- heat with or without any rolling or compacting devices 212 can be used to flatten the pellets 204 and/or form the lime layer 214.
- the second asphalt layer 206 can be deposited thereon.
- the lime layer 214 can be used to enhance the bonding between the first asphalt layer 202 and the second asphalt layer 206. While embodiments of processes for adhering asphalt layers together with lime pellets have been depicted and described, it should be appreciated that other variations to such processes can be made within the scope of the invention.
- a series of pellets having varying compositions are prepared in accordance with the protocol of Example 1 with minor modifications. Briefly, varying compositions of liquefied hydrophobic binder are added drop-wise to the lime fines (calcium hydroxide and/or calcium oxide). The feed rates of lime and/or binder are modified in order to alter pellet sizes and compositions.
- a lime-based pellet is prepared using a disc pelletizer and associated method as described in Example 1. Briefly, a supply of lime fines combined with manganese oxide is added to the rotating disc of a disc pelletizer, and liquefied brewer's starch is added drop-wise. Pellets are formed by contacting the brewer's starch with the lime fines. The average size of the pellets is expected to be 1.27 cm with a composition of 97% lime fines, 1% brewer's starch, and 2% manganese oxide.
- a series of pellets having varying compositions are prepared in accordance with the protocol of Example 1 with minor modifications. Briefly, varying compositions of tall oil pitch are combined with lime fines (calcium hydroxide and/or calcium oxide). The expected shape, size (average diameter), and compositions of the pellets are described in Table 3 as follows: TABLE 3 Component % (by weight) PELLET 24 Spheroid (2 cm) Calcium hydroxide 98 Tall oil pitch 1 Manganese oxide 1 PELLET 25 Spheroid (1.3 cm) Calcium hydroxide 90 Tall oil pitch 5 Styrene-butadiene-styrene 3 Manganese oxide 2 PELLET 26 Spheroid (1.5 cm) Calcium hydroxide 80 Tall oil pitch 10 Styrene-butadiene rubber 5 Phosphorus oxide 2 Manganese oxide 3 PELLET 27 Spheroid (0.8 cm) Calcium hydroxide 70 Tall oil pitch 15 Fly ash 8 Potassium chloride 5 Manganese oxide 2 PELLET 28 Spheroid (0.5 cm) Calcium hydroxide 60 Tall oil pitch 20 Sty
- the rate of dissolution of the lime-based pellets formed with a hydrophobic binder prepared in accordance to Example 2 is determined by addition to mineral oil (Sigma-Aldrich) heated to 150°C. Briefly, a pellet having a dark color is placed into 250 ml of transparent mineral oil in a 500 ml open-mouth flask and stirred with a magnetic stir bar under heat. The pellet is observed to decrease in size until it is unobservable. When the pellet is unobservable, it is considered to be substantially dissolved.
- the expected time (seconds) in order for each pellet to become substantially dissolved is provided in Table 4 as follows: TABLE4 Pellet Dissolution Rate (s) 1 6 2 11 3 16 4 12 5 19 6 27 7 8 8 12 9 7 10 12 12 14
- the rate of dissolution of the lime-based pellets formed with a hydrophilic binder prepared in accordance to Example 3 is determined by addition to water heated to 100°C (212°F).
- the expected time (seconds) in order for each pellet to become substantially dissolved is provided in Table 5 as follows: TABLE 5 Pellet Dissolution Rate (s) 13 10 14 8 15 16 16 21 17 17 18 5 19 9 20 7 21 6 22 5 23 12
- pellets having a composition according to Pellet 11 of Example 2 are determined to assess resistance to degradation and agglomeration. Briefly, pellets having the characteristics of Pellet 11 are placed into a 500 ml open-mouth flask and stored in ambient conditions. The resistance to agglomeration and degradation are observed periodically up to 6 months. It is expected that the pellets will not substantially degrade or agglomerate at any time up to the 6-month period.
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Claims (8)
- Granulat für eine heiße Asphaltmischung,
das folgendes aufweist:- Kalkfeinstoffe mit einem Anteil von mehr als 1 %, und zwar auf das Gesamtgewicht des Granulats bezogen;- wobei der Begriff "Kalk" für Calciumhydroxid und/oder Calciumoxid, jedoch nicht für Kalkstein steht;- ein hydrophobes Bindemittel, das die Kalkfeinstoffe zu Granulat bindet, mit einem Anteil von 0,5 bis 69 %, und zwar auf das Gesamtgewicht des Granulats bezogen, wobei das hydrophobe Bindemittel zumindest eines der folgenden aufweist: ein Polymer in Form eines Elastomers, ein Polymer in Form eines Plastomers, Tallölpech oder Asphaltzement,wobei das Bindemittel dadurch gekennzeichnet ist,
dass weniger als 50 Gew.-% des gesamten Bindemittels Schwefel sind, und wobei das Granulat dadurch gekennzeichnet ist,
dass es eine Abmessung von mehr als 1,5 mm aufweist;
wobei die Kalkfeinstoffe im wesentlichen aus Calciumhydroxid oder Calciumoxid bestehen, die in einer Menge von mehr als 31 Gew.-% vorliegen. - Granulat nach Anspruch 1,
wobei das hydrophobe Bindemittel ferner zumindest eine der folgenden Substanzen aufweist: Bitumen, schweres Rohöl, Heizöl, Acrylpolymere, Silicium aufweisende Polymere oder Latices. - Granulat nach Anspruch 2,
wobei das hydrophobe Bindemittel ferner einen Zusatz aufweist, wobei der Zusatz mit weniger als 30 % des Gesamtgewichts des Granulats vorliegt und zumindest eine der folgenden Substanzen aufweist: aliphatisches Erdöldestillat, Latices, Calciumchlorid, Manganoxid, Styrol-Butadien-Styrol-Copolymere, Styrol-Ethylen/Butylen-Styrol-Copolymere, Styrol-Isopren-Copolymere, Styrol-Ethylbutylen-Copolymere, Styrol-Butadien-Kautschuklatices, Polychloropren-Latices, Polyisoprene, Polyethylenacetate, Polyethylene, Polypropylene und auf Silicium basierende Polymere. - Verfahren zum Herstellen des Kalkgranulats nach Anspruch 1,
wobei das Verfahren folgendes aufweist:- Mischen der Kalkfeinstoffe mit dem hydrophoben Bindemittel und- Erzeugen von Granulat, das Kalkfeinstoffe und hydrophobes Bindemittel aufweist, wobei das Granulat dadurch gekennzeichnet ist,
dass es für mehr als ein Jahr lagerbeständig ist. - Verfahren nach Anspruch 4,
wobei das Granulat im wesentlichen eine Form hat, die aus der Gruppe ausgewählt ist, die aus Sphäroiden, Pastillen, Würfeln, Platten und Kombinationen davon besteht. - Verfahren nach Anspruch 5,
wobei das Bindemittel zumindest eine der folgenden Substanzen aufweist:Bitumen, Tallölpech, Asphaltzement, schweres Rohöl, Heizöl, Acrylpolymere, Silicium aufweisende Polymere oder Latices. - Verfahren nach Anspruch 6,
das ferner das Mischen eines weiteren Bestandteils mit den Kalkfeinstoffen und dem mit Asphalt kompatiblen Bindemittel aufweist, wobei der weitere Bestandteil zumindest einer der folgenden ist: ein Salz, ein Viskositätsveränderer, Sand, Siliciumdioxid, Flugasche, Keramikteilchen, Glasteilchen, Tonteilchen, pozzuolanartige Materialien, Füllstoffe, Lösungsmittel oder Farbe verleihende Mittel. - Granulat nach Anspruch 1,
wobei das hydrophobe Bindemittel mit 25 % bis 69 % im Granulat enthalten ist, und zwar auf das Gesamtgewicht des Granulats bezogen.
Priority Applications (1)
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EP14177971.0A EP2860224B1 (de) | 2005-05-20 | 2006-05-19 | Pelletierung von Kalkfeingut mit asphaltverbessernden Bindemitteln und Verfahren zur Verwendung bei der Herstellung von Asphalt |
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US11/134,797 US7303623B2 (en) | 2005-05-20 | 2005-05-20 | Pelleting lime fines with asphalt enhancing binders and methods of use in asphalt manufacturing |
PCT/US2006/019874 WO2006127683A2 (en) | 2005-05-20 | 2006-05-19 | Pelleting lime fines with asphalt enhancing binders and methods of use in asphalt manufacturing |
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EP14177971.0A Division EP2860224B1 (de) | 2005-05-20 | 2006-05-19 | Pelletierung von Kalkfeingut mit asphaltverbessernden Bindemitteln und Verfahren zur Verwendung bei der Herstellung von Asphalt |
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EP1885660A2 EP1885660A2 (de) | 2008-02-13 |
EP1885660A4 EP1885660A4 (de) | 2011-05-25 |
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EP14177971.0A Active EP2860224B1 (de) | 2005-05-20 | 2006-05-19 | Pelletierung von Kalkfeingut mit asphaltverbessernden Bindemitteln und Verfahren zur Verwendung bei der Herstellung von Asphalt |
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SU985095A1 (ru) * | 1981-08-14 | 1982-12-30 | Ордена Трудового Красного Знамени Научно-Исследовательский И Проектный Институт Обогащения И Механической Обработки Полезных Ископаемых "Уралмеханобр" | Св зующее дл окусковани металлургических шихт |
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-
2005
- 2005-05-20 US US11/134,797 patent/US7303623B2/en not_active Expired - Fee Related
-
2006
- 2006-05-19 WO PCT/US2006/019874 patent/WO2006127683A2/en active Application Filing
- 2006-05-19 EP EP06760293.8A patent/EP1885660B1/de active Active
- 2006-05-19 EP EP14177971.0A patent/EP2860224B1/de active Active
- 2006-05-19 CA CA2608867A patent/CA2608867C/en not_active Expired - Fee Related
-
2007
- 2007-11-08 US US11/937,305 patent/US7517401B2/en not_active Expired - Fee Related
Cited By (1)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
DE102016010260A1 (de) | 2015-08-28 | 2017-03-02 | Andreas Rupprecht | Gerät mit einem Einstrom - Strahltriebwerk zur Bearbeitung von Verkehrsflächen |
Also Published As
Publication number | Publication date |
---|---|
CA2608867C (en) | 2011-11-08 |
EP1885660A4 (de) | 2011-05-25 |
US7303623B2 (en) | 2007-12-04 |
WO2006127683A3 (en) | 2007-03-01 |
CA2608867A1 (en) | 2006-11-30 |
EP2860224A1 (de) | 2015-04-15 |
EP1885660A2 (de) | 2008-02-13 |
US20080223257A1 (en) | 2008-09-18 |
EP2860224B1 (de) | 2019-02-27 |
WO2006127683A2 (en) | 2006-11-30 |
US7517401B2 (en) | 2009-04-14 |
US20060260508A1 (en) | 2006-11-23 |
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